Processes and systems for using silica particles in fluid bed reactor
The present disclosure relates to fluid bed processes that utilize silica particles as a fluidization aid. The process comprises reacting one or more reactants in a reactor comprising a fluid bed to form a product. The fluid bed comprises a catalyst composition comprising a catalyst and an inert additive composition comprising silica particles from 0.5 wt % to 30 wt %, based on the total weight of the catalyst composition. The silica particles are discrete, inert particles that are mixed with the catalyst in the fluid bed.
1. A process comprising:
reacting one or more reactants in a reactor comprising a fluid bed to form a product;
wherein the one or more reactants are passed upwardly through the fluid bed,
wherein the fluid bed comprises a catalyst composition comprising a catalyst and an inert additive composition comprising from 0.5 wt % to 30 wt % of silica particles, based on the total weight of the catalyst composition,
wherein the silica particles have an equivalent median particle diameter ranging from 10 microns to 500 microns,
wherein a difference between the density of the silica particles and catalyst particles ranges from 0.5% to 75%,
wherein the silica particles have a real density ranging from 1.8 g/cm 3 to 2.8 g/cm 3 .
2. The process of claim 1 , wherein the catalyst comprises one or more of antimony, uranium, iron, bismuth, vanadium, molybdenum, nickel, potassium, cobalt, oxides thereof, or salts thereof.
3. The process of claim 1 , wherein the catalyst has an equivalent median diameter ranging from 1 microns to 125 microns.
4. The process of claim 1 , wherein the difference between the density of the silica particles and the catalyst is less than 75%.
5. The process of claim 1 , wherein the silica particles have a surface area less than 50 m 2 /g, and wherein the silica particles have a hardness ranging from 500 to 720 as measured by ASTM E384 (2018).
6. The process of claim 1 , wherein the silica particles have a sphericity ranging from 60% to 99.9%.
7. The process of claim 1 , wherein the catalyst composition further comprises alumina particles, wherein a weight ratio of alumina particles to silica particles is less than 1:1.
8. The process of claim 1 , wherein the inert additive composition comprises no alumina.
9. The process of claim 1 , wherein the process reduces consumption of the catalyst by greater than 5% per kilogram of the acrylonitrile produced compared to other fluidization aids.
10. The process of claim 1 , wherein the silica particles reduce erosion of the reactor by greater than 10% compared to a similar process conducted without from 0.5 wt % to 30 wt % silica particles.
11. The process of claim 1 , wherein the process demonstrates an acrylonitrile yield greater than 0.2% greater than that of a similar process conducted without from 0.5 wt % to 30 wt % silica particles.
12. The process of claim 1 , wherein the silica particles have a real density ranging from 2.1 g/cm 3 to 2.5 g/cm 3 , wherein the silica particles have a surface area less than 1 m 2 /g, wherein the silica particles have a hardness ranging from 500 to 720 as measured by ASTM E384 (2018), and wherein the acrylonitrile yield is greater than 70%.
13. The process of claim 1 , wherein the silica particles have an equivalent median particle diameter ranging from 20 microns to 100 microns, wherein the silica particles have a real density ranging from 2.1 g/cm 3 to 2.5 g/cm 3 , wherein the silica particles have a sphericity greater than 67%, wherein the silica particles comprise greater than 99 wt % silica, wherein the acrylonitrile yield is greater than 70%.
14. A process for producing acrylonitrile product, the process comprising:
reacting one or more reactants in a reactor comprising a fluid bed to form acrylonitrile;
wherein the one or more reactants are passed upwardly through the fluid bed,
wherein the fluid bed comprises a catalyst composition comprising a catalyst and an inert additive composition comprising silica particles having a density from 1.8 g/cm 3 to 2.8 g/cm 3 ,
wherein the silica particles have a sphericity ranging from 60% to 99.9%.
15. The process of claim 14 , wherein the difference between the density of the silica particles and the catalyst is less than 75%, wherein the process demonstrates an acrylonitrile yield greater than 0.2% greater than that of a similar process conducted without silica particles.
16. The process of claim 14 , wherein the one or more reactants comprises an olefin, ammonia, and an oxygen-containing gas.
17. The process of claim 1 , wherein the silica particles reduce erosion of the reactor by greater than 10% compared to a process conducted without from 0.5 wt % to 30 wt % silica particles.
18. A reactor system for preparing acrylonitrile, comprising:
a fluid bed comprising a catalyst composition comprising a catalyst and an inert additive composition comprising from 0.5 wt % to 30 wt % of silica particles, based on the total weight of the catalyst composition; and
one or more gas inlet feeds for passing one or more reactants upwardly through the fluid bed to form acrylonitrile,
wherein the difference between the density of the silica particles and the catalyst particles ranges from 0.5% to 75%,
wherein the silica particles reduce erosion of the reactor by greater than 10% compared to a process conducted without from 0.5 wt % to 30 wt % silica particles,
wherein the silica particles have a real density ranging from 1.8 g/cm 3 to 2.8 g/cm 3 .
19. The system of claim 18 , wherein the silica particles have a surface area less than 50 m 2 /g, wherein the silica particles have a hardness ranging from 500 to 720 as measured by ASTM E384 (2018), and wherein the acrylonitrile yield is greater than 70%.
20. The system of claim 18 , wherein the process demonstrates an acrylonitrile yield greater than 0.2% greater than that of a process conducted without from 0.5 wt % to 30 wt % silica particles.
21. The system of claim 18 , wherein the reactor system further comprises:
one or more cyclones to separate particles from the gas flowing upwardly through the fluid bed of the reactor, the cyclones being in communication with the upwardly flowing gas exiting the fluid bed, wherein the one or more cyclones comprise a particle discharge pipe for returning separated particles to the fluid bed.
22. A reactor system for preparing acrylonitrile, comprising:
a fluid bed comprising a catalyst composition comprising a catalyst and an inert additive composition comprising from 0.5 wt % to 30 wt % of silica particles, based on the total weight of the catalyst composition; and
one or more gas inlet feeds for passing one or more reactants upwardly through the fluid bed to form acrylonitrile,
wherein the difference between the density of the silica particles and the catalyst particles ranges from 0.5% to 75%,
wherein the silica particles reduce erosion of the reactor by greater than 10% compared to a process conducted without from 0.5 wt % to 30 wt % silica particles,
wherein the silica particles have a sphericity ranging from 60% to 99.9%.
23. The system of claim 18 , wherein the silica particles have a real density ranging from 2.1 g/cm 3 to 2.5 g/cm 3 , wherein the silica particles have a surface area less than 1 m 2 /g, wherein the silica particles have a hardness ranging from 500 to 720 as measured by ASTM E384 (2018), and wherein the acrylonitrile yield is greater than 70%.
24. The system of claim 18 , wherein the silica particles have an equivalent median particle diameter ranging from 20 microns to 100 microns, wherein the silica particles have a real density ranging from 2.1 g/cm 3 to 2.5 g/cm 3 , wherein the silica particles have a sphericity greater than 67%, wherein the silica particles comprise greater than 99 wt % silica, and wherein the acrylonitrile yield is greater than 70%.